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US3209044A Expired / Lapsed US ⏱️ 0.0 years remaining

C8 aromatics processing

Assignee: Total Petrochemicals and Refining USA Inc
•
Filing: 1961-04-21
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Granted: 1965-09-28
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Expires: 1981-04-21
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Abstract

No abstract record available.

Inventors

  • 👤 Meek Paul Derald
  • 👤 Mayes Warden William
  • 👤 Jenkins Jerry Gray

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 20:51
CPC Classifications
C; C07; C07C; C07C15/00; C07C15/40; C07C15/42; C07C15/44; C07C15/46; C07C7/00; C07C7/04

Claims Analysis

Total Claims: 2
Claim 1
Independent Claim 146 words
IN THE PREPARATION OF STYRENE FROM A MIXTURE OF ETHYLBENZENE, XYLENE ISOMERS AND NON-AROMATIC HYDROCARBON COMPONENTS, THE STEPS OF PREFRACTIONATING THE MIXTURE TO FORM C8 AROMATICS CONTAINING A LARGE QUANTITY FROM ABOUT 1% TO ABOUT 5% OF NON-AROMATIC COMPONENTS BOILING IN ABOUT THE C8 AROMATIC HYDROCARBON BOILING RANGE, SUPERDISTILLING THE SAID HYDROCARBON MIXTURE IN A DISTILLATION COLUMN OF AT LEAST 150 DISTILLATION STAGES AND AT A REFLUX RATIO EXCEEDING 40:1 TO SEPARATE THE XYLENES AND PASSING THE MIXTURE OF PURE ETHYL BENZENE AND NONAROMATIC HYDROCARBON MIXTURE TO A DEHYDROGENATION REACTOR TO CONVERT THE ETHYL BENZENE TO STYRENE IN THE PRESENCE OF SAID NON-AROMATIC HYDROCARBON, SEPARATING SUBSTANTIALLY PURE STYRENE FROM THE CRUDE DEHYDROGENATION REACTION MIXTURE BY DISTILLATION AND RECYCLING AT LEAST A PORTION OF SAID UNREACTED MIXTURE OF ETHYL BENZENE AND NON-AROMATIC HYDROCARBON TO SAID PREFRACTIONATOR IN QUANTITY SUFFICIENT TO PREVENT LARGE NON-AROMATIC ACCUMULATION IN THE SYSTEM.
Claim 2
Dependent Claim 146 words
IN THE PREPARATION OF STYRENE FROM A MIXTURE OF ETHYLBENZENE, XYLENE ISOMERS AND NON-AROMATIC HYDROCARBON COMPONENTS, THE STEPS OF PREFRACTIONATING THE MIXTURE TO FORM C8 AROMATICS CONTAINING A LARGE QUANTITY FROM ABOUT 1% TO ABOUT 5% OF NON-AROMATIC COMPONENTS BOILING IN ABOUT THE C8 AROMATIC HYDROCARBON BOILING RANGE, SUPERDISTILLING THE SAID HYDROCARBON MIXTURE IN A DISTILLATION COLUMN OF AT LEAST 150 DISTILLATION STAGES AND AT A REFLUX RATIO EXCEEDING 40:1 TO SEPARATE THE XYLENES AND PASSING THE MIXTURE OF PURE ETHYL BENZENE AND NONAROMATIC HYDROCARBON MIXTURE TO A DEHYDROGENATION REACTOR TO CONVERT THE ETHYL BENZENE TO STYRENE IN THE PRESENCE OF SAID NON-AROMATIC HYDROCARBON, SEPARATING SUBSTANTIALLY PURE STYRENE FROM THE CRUDE DEHYDROGENATION REACTION MIXTURE BY DISTILLATION AND RECYCLING AT LEAST A PORTION OF SAID UNREACTED MIXTURE OF ETHYL BENZENE AND NON-AROMATIC HYDROCARBON TO SAID PREFRACTIONATOR IN QUANTITY SUFFICIENT TO PREVENT LARGE NON-AROMATIC ACCUMULATION IN THE SYSTEM.

References Cited (Backward Citations)

US2064571A Cited
US2282231A Cited
US2404104A Cited
US2467152A Cited
GB603497A Cited
US2447479A Cited
GB646116A Cited
US2959626A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1968-09-27 1969-03-29 1969-09-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1972-09-27 1973-03-29 1973-09-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1976-09-27 1977-03-29 1977-09-28 $7700.00 Window Closed / Lapsed

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